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Hydrotreatment catalyst and its preparation method

A hydrogenation treatment and catalyst technology, applied in physical/chemical process catalysts, chemical instruments and methods, metal/metal oxide/metal hydroxide catalysts, etc., can solve the problems of crude oil becoming heavier and worse

Active Publication Date: 2012-11-07
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In addition, due to the reduction of oil resources, the nature of crude oil has become heavier and worse, and refineries have to process lower-quality crude oil

Method used

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  • Hydrotreatment catalyst and its preparation method
  • Hydrotreatment catalyst and its preparation method
  • Hydrotreatment catalyst and its preparation method

Examples

Experimental program
Comparison scheme
Effect test

example 1

[0039] Take by weighing 2000 grams of aluminum hydroxide powder (dried rubber powder produced by Changling Branch Catalyst Factory, dry basis 72% by weight), extrude into a butterfly bar with a circumscribed circle diameter of 1.3 mm with an extruder, and wet the bar at 120 ° C Drying for 4 hours and calcining at 600° C. for 3 hours to obtain carrier S1.

[0040] Take by weighing 50 grams of ammonium molybdate (Tianjin, analytically pure) and join in 120 milliliters of water, add dropwise the ammoniacal liquor that concentration is 25% to ammonium molybdate and dissolve under heating and stirring, then add 30 grams of cobalt nitrate (Beijing, analytically pure), stir After dissolving, add 20 milliliters of ethanol (Beijing, analytically pure), add water to 200 milliliters, impregnate 100 grams of carrier S1 in excess, and place the system in a synthesis reactor for reaction for 4 hours. The reaction conditions include: temperature 150 ° C, pressure 0.7MPa, where, P 0 =0.5MPa,...

example 2

[0042] Weigh 15 grams of basic cobalt carbonate (Jiangxi, analytically pure) and 30 grams of molybdenum trioxide (Tianjin, analytically pure) and add them to 120 milliliters of water, add 10 grams of phosphoric acid (Beijing, analytically pure) under stirring, heat and stir to dissolve, add 15 milliliters of isopropanol (Tianjin, analytically pure), add water to 200 milliliters, excessively impregnate 100 grams of carrier S1, and place the system in a synthesis reactor for 10 hours of reaction. The reaction conditions include: temperature 200 ° C, pressure 2.1 MPa , where P 0 =1.5MPa, ΔP=0.6MPa, after cooling and filtering, the obtained sample was dried at 120°C for 2 hours and calcined at 250°C for 3 hours to obtain catalyst B-2. The composition of catalyst B-2 is shown in Table 1.

example 3

[0044] Take by weighing basic nickel carbonate (Shensheng, analytical pure) 20 grams and join in 150 milliliters of water, add 8 grams of phosphoric acid (Beijing, analytical pure) under stirring, heat and stir to dissolve, add ammonium molybdate (Tianjin, analytical pure) respectively under stirring ) 12 grams, ammonium metatungstate (Sichuan, analytically pure) 110 grams, add water to 200 milliliters, excessively impregnate 100 grams of carrier S1, and place the system in a synthesis reactor for 24 hours of reaction. The reaction conditions include: temperature 100 ° C , introducing nitrogen to make the reaction pressure 5.2MPa, where, P 0 =0.2MPa, ΔP=5.0MPa, after cooling and filtering, the obtained sample was dried at 120°C for 2 hours and calcined at 200°C for 3 hours to obtain catalyst B-3. The composition of catalyst B-3 is shown in Table 1.

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Abstract

Disclosed are a hydrotreatment catalyst and its preparation method. The catalyst is prepared by the following steps of: (1) preparing a dipping solution containing at least one VIII group metal component containing compound and at least one VIB group metal component containing compound; (2) dipping a carrier by the use of the dipping solution prepared in the step (1) to obtain a mixture of the dipping solution and the carrier; (3) placing the dipping solution and carrier containing mixture obtained from the step (2) into a reactor for reaction, while the reaction conditions are: the temperature is 100-200 DEG C, the pressure is P0+delta P, and the time is 0.5-36 hours; and (4) adopting drying, roasting or non-roasting method on the product obtained from the step (3) to prepare the catalyst, wherein P0 is the reaction pressure under standard condition and delta P is 0.05-15 MPa. In comparison with catalysts in the prior art, the catalyst prepared by the method has a higher hydrogenation activity.

Description

technical field [0001] The present invention relates to a hydrotreating catalyst and a preparation method thereof. Background technique [0002] With the increasingly stringent environmental protection requirements around the world, countries have increasingly stringent requirements on the quality of vehicle fuels. In addition, due to the reduction of oil resources, the properties of crude oil have become heavier and worse, and refiners have to process crude oil of lower quality. Therefore, greatly reducing the content of impurities and polycyclic aromatic hydrocarbons in diesel oil and significantly improving the quality of diesel oil has become an urgent problem for refiners to solve. Hydrogenation technology is one of the main technologies to reduce the impurity content of oil products and improve the quality of oil products, and its core is hydrogenation catalyst. SUMMARY OF THE INVENTION [0003] The technical problem to be solved by the present invention is to prov...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/882B01J23/888C10G45/08
Inventor 张乐龙湘云刘学芬刘清河李明丰聂红李大东陈若雷
Owner CHINA PETROLEUM & CHEM CORP